Indirect Heat Exchanger Pressure Vessel with Controlled Wrinkle Bends
In one aspect of the present disclosure, an indirect heat exchanger pressure vessel is provided that includes an inlet header to receive a pressurized working fluid, such as water, glycol, ammonia, and/or CO2. The indirect heat exchanger pressure vessel includes an outlet header to collect the pressurized working fluid and a serpentine circuit tube connecting the inlet and outlet headers. The serpentine circuit tube permits the pressurized working fluid to flow from the inlet header to the outlet header. The serpentine circuit tube includes runs and a return bend connecting the runs. The return bend has a controlled wrinkled portion comprising alternating ridges and grooves. The alternating ridges and grooves strengthen the return bend and permit the indirect heat exchanger pressure vessel to facilitate working fluid heat transfer at a high internal operating pressure.
This application claims the benefit of U.S. Provisional Patent Application No. 63/138,655, filed Jan. 18, 2021, and U.S. Provisional Patent Application No. 63/270,953 filed, Oct. 22, 2021, which are hereby incorporated herein by reference in their entireties.
FIELDThis disclosure relates to indirect heat exchangers and, more particularly, to indirect heat exchangers having serpentine circuit tubes with multiple formed bends that convey a pressurized working fluid through the serpentine circuit tube and permit heat transfer between the working fluid inside of the serpentine circuit tube and a fluid external to the serpentine circuit tube. The working fluid and the external fluid may each be gas, liquid or a mixture of gas and liquid.
BACKGROUNDHeat exchangers are known that include direct heat exchangers and indirect heat exchangers. A direct heat exchanger transfers heat between a working fluid and another fluid via contact between the fluids. An indirect heat exchanger transfers heat between a working fluid and another fluid indirectly through a medium separating the fluids.
Various types of heat exchange apparatuses are known that include direct heat exchangers, indirect heat exchangers, or both. Known heat exchange apparatuses include open circuit heat exchange apparatuses such as open circuit cooling towers and closed circuit heat exchange apparatuses such as closed circuit cooling towers. Open circuit cooling towers may exchange heat between a working fluid, such as water, and an external fluid such as ambient air by distributing the working fluid onto fill. The working fluid is directly cooled by ambient air as the working fluid travels along the fill. Closed circuit cooling towers, by contrast, keep the working fluid separated from the external fluid.
Closed circuit heat exchanger apparatuses include closed circuit cooling towers for fluids, evaporative condensers for refrigerants, dry coolers, air cooled condensers, and ice thermal storage systems. These heat exchange apparatuses utilize one or more heat exchangers to transfer heat between a pressurized working fluid and an external fluid such as ambient air, an evaporative liquid, or a combination thereof.
For example, a heat exchanger apparatus may include a closed circuit cooling tower having an indirect heat exchanger pressure vessel including an inlet header that receives a pressurized working fluid, an outlet header, and an indirect heat exchange coil connecting the inlet and outlet headers. The indirect heat exchange coil may include one or more serpentine circuit tubes configured to transfer heat between the pressurized working fluid inside the indirect heat exchange coil and a fluid, such as an evaporative liquid, external to the indirect heat exchange coil. The inlet header receives the internal working fluid from an upstream component of the heat exchange apparatus and the outlet header collects the pressurized working fluid before the working fluid is directed to a downstream component of the heat exchange apparatus.
Indirect heat exchanger pressure vessels, which includes the inlet header, outlet header, and one or more serpentine circuit tubes, are required to withstand high pressures appropriate for the specific application and satisfy domestic and international engineering standards such as ASME Standard B31.5. For example, an indirect heat exchanger pressure vessel of a closed circuit cooling tower may be rated to withstand an internal pressure of 150 psig for fluids such as water, glycols and brines. As another example, the indirect heat exchanger pressure vessel of an evaporative condenser may be able to withstand an internal pressure of up to 410 psig or higher for typical refrigerants such as ammonia or R-407C. As yet another example, some evaporative condensers have indirect heat exchanger pressure vessels with internal pressure ratings of 1200 psig or greater for refrigerants such as CO2.
Serpentine circuit tubes of indirect heat exchanger pressure vessels typically include straight lengths and bends connecting the straight lengths. The straight lengths of the serpentine circuit tubes are typically joined with bends of approximately 180 degrees or by compound bends having multiple bends, such as two 90 degree bends joined by a tube length.
The serpentine circuit tubes may be stacked together during assembly of the heat exchange apparatus with the serpentine circuit tubes contacting one another, typically in the area of the return bends, and with the serpentine circuit tubes having a vertically staggered positioning.
Serpentine circuit tubes are often made by first forming an elongated tube from a long, flat strip of metal such as mild steel or stainless steel. The flat strip of metal is roll formed into a generally circular cross section and the longitudinal edges are welded together with a continuous, longitudinal weld to form a straight tube. In another approach, a seamless tube forming process is used to form the straight tube. The resulting straight tube may then be bent at spaced locations along the tube to form the tube into a serpentine shape with straight runs connected by bends. Tube bending is a complicated process and often utilizes a hydraulically, electrically, or manually-powered tube bender having a bend die, a clamp die, a pressure die, and optionally a mandrel and wiper die. The tube bender may be setup to form bends with any desired angle up to and including 180 degree bends, such as 80 degrees, 90 degrees, 100 degrees, or 180 degrees. As noted above, the return bends of a serpentine circuit tube may include compound bends each having two or more bends, such as an 80 degree bend and a 100 degree bend, connected by a length of straight tube.
To form a bend in a tube, the tube is fed into the tube bender and a portion of the tube is nestled in a recess of the bend die. The pressure die and clamp die, with recesses for the tube, are moved against the opposite side of the tube such that the pressure die is positioned to support the tube and the clamp die clamps the tube portion between the clamp die and the bend die. The tube bender then rotates or pivots the bend die and the clamp die through the desired bend angle. The pressure die moves forward as the bend die and clamp die pivot to support the tube and ensure the tube follows the profile of the bend die. Once the bend has been formed in the tube, the clamp die and pressure die retract from their clamped positions, the tube is fed forward until the next bend location of the tube is positioned in the tube bender, and the bend die, clamp die, and pressure die all move back to their initial positions. The bending process is repeated for each bend to be formed in the serpentine circuit tube. Some tubes are bent only once to form single-bend tubes, which commonly are referred to as hairpin or candy-cane tubes, that can be subsequently butt welded together.
The bending of a tube that is to receive a pressurized working fluid is a process that balances various considerations including performance, safety, and packaging criteria for a particular application. Further, unintended deformations in the tube wall during the bending process may lead to tube failures due to the pressure of the working fluid within the tube, corrosion of the tube, and/or a higher pressure drop of the working fluid through the tube. In some tube bending processes, an internal mandrel is advanced into the interior of the tube to support the tube wall during bending and a wiper die may be used to stiffen the tube wall at a trailing end of the inside of the bend to prevent unintended deformations in the tube. The internal mandrel may be a plug mandrel or may have one or more balls or rings, in which case the internal mandrel is referred to as a ball mandrel.
Tube bending generally involves the following parameters:
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- OD=Outside diameter of the tube
- WT=Wall thickness of the tube
- CLR=Centerline radius of the bend
The dimensions are measured using a common measurement scale, such as inches or millimeters. These parameters are used to calculate the following two characteristic ratios:
Two other parameters that are featured in the bending process are the Outside Radius (OSR) of the bend, usually referred to as the extrados, and the Inside Radius (ISR) of the bend, usually referred to as the intrados.
The W and D ratios are further consolidated into a single factor that is indicative of the complexity of the bend. This factor is calculated as:
The values of W, D, and/or CB may be used to determine whether a bend can be formed without an internal mandrel, called empty bending, or if an internal mandrel will be required, in which case the process is called mandrel bending. For mandrel bending, these ratios help determine whether the internal mandrel required should be a multiple ball, single ball or a simpler plug mandrel. Finally, these ratios help determine whether a wiper die will be required in combination with the internal mandrel. As an example, process recommendations for various bend complexities are shown in the table below:
It is typical to look up the W, D, and/or CB ratios on industry standard tube bending charts to decide the type of bending process required. For example, to determine the process parameters to bend a tube with outside diameter of 1″ and a wall thickness of 0.05″ with a centerline radius of 2″, then the ratios W and D are:
An industry standard tube bending chart may recommend, in view of the W ratio of 20 and the D ratio of 2, that a regular pitch internal mandrel with 1 ball, supplemented with a wiper die, should be used.
Alternately, the CB for the example bend above is:
Referring to the table above, this CB value also indicates that an internal mandrel is recommended, although a wiper die could be optional. The small differences in recommendations on mandrels and wipers are indicative of a certain amount of flexibility in bend configurations where tool design and tube material choices can sometimes compensate for the absence of an internal mandrel and/or wiper die.
The conventional bending charts used in industry and the bend complexity value (CB) ranges discussed above are based on the assumption that the profile of the tooling groove formed by the bending and clamp dies, where the tube is seated during the bending process, is circular, complementing the shape of the round tube. However, bending tool design has made several advances in recent years and it is possible to design bend tooling with a composite radius in the tooling groove to compress and support the tube during the bending process and extend the range of empty bending up from a CB value of approximately 5 to approximately 12.
Beyond this, especially as CB approaches and exceeds 20, it becomes progressively more necessary to use internal mandrels and wiper dies to successfully bend the tube. The internal mandrel bending process has several disadvantages including that using a mandrel requires additional tooling which adds cost, may increase scrap if mandrels are not used correctly, may add to cycle time, and requires the use of lubricants which adds time and cost for the lubricant and subsequent environmental mitigation.
One issue as CB approaches and exceeds 20 is that the associated mandrel bending imposes a limit on the continuous length of the tube. Serpentine circuit tubes can be very long, up to 400 feet long for some applications. The physical limits on the length of the mandrel rod and setup mean that internal mandrels cannot be used to bend long, continuous serpentine circuit tubes with several bends. This forces a manufacturer to form one or two bends in short segments of tube, sometimes called candy canes, and then butt weld the tube segments together to create larger circuits. Not only does this involve additional labor and cost, but additional butt welds increase the possibility of leaks and may not be permitted in many applications due to the high operating pressure the serpentine circuit tube will experience.
Another issue that may arise as CB approaches and exceeds 20 is that the associated internal mandrel bending moves the neutral axis of the bend closer to the inside of the bend and may cause excessive thinning of the outside wall portion of the bend. Thinning of the outside wall portion of the bend may weaken the serpentine circuit tube such that the serpentine circuit tube cannot withstand the pressure of the working fluid for a particular application. Excessive thinning of the outside bend wall also creates variability in the process when forming the bends causing reduced quality in the bend areas.
The above issues make it desirable for a manufacturer to avoid the use of internal mandrels for tube bending. One way to avoid using internal mandrels for a tube with a given OD is to increase WT or increase CLR to a suitable value to bring the bend within the range of empty bending. Increasing the wall thickness (WT) may not be an option for manufacturers whose products do not require such relatively thick walls from an operational perspective. In certain cases, the thicker walls may increase the fluid side pressure drop, may make the products less thermally efficient, increase the weight of the assembly, and may increase the material cost of the serpentine circuit tube. Further, increasing CLR may not be an option where the serpentine circuit tube needs to fit in a given space for other operational considerations. Increasing CLR can also have negative impact on overall coil thermal and hydraulic efficiency in some cases.
SUMMARYIn one aspect of the present disclosure, an indirect heat exchanger pressure vessel is provided that includes an inlet header to receive a pressurized working fluid, an outlet header to collect the pressurized working fluid, and a serpentine circuit tube connecting the inlet and outlet headers and permitting the pressurized working fluid to flow from the inlet header to the outlet header. The pressurized fluid may be, for example, water, glycol, a glycol mixture, ammonia, or CO2 as some examples. The pressurized fluid may be a liquid such as water or a liquid/gas combination such as refrigerant liquid and refrigerant vapor. The serpentine circuit tube includes runs and a return bend connecting the runs. The return bend includes a controlled wrinkled portion including alternating ridges and grooves. The controlled wrinkled portion of the return bend provides a rigid structure that resists internal pressure during operation of the indirect heat exchanger pressure vessel. Further, the controlled wrinkled portion provides a constructive bend centerline radius that is larger than an actual bend centerline radius of the return bend. The larger constructive bend centerline radius reduces the bend complexity factor for the return bend compared to a return bend of a conventional serpentine circuit tube having the same outer diameter and wall thickness. Due to the reduced bend complexity factor, the return bend having controlled wrinkled portions may be bent without the use of an internal mandrel which simplifies the manufacturing process of the serpentine circuit tube.
The present disclosure also provides an indirect heat exchanger pressure vessel including an inlet header to receive a pressurized working fluid, an outlet header to collect the pressurized working fluid, and a serpentine circuit tube connecting the inlet and outlet headers to permit flow of pressurized working fluid from the inlet header to the outlet header. The serpentine circuit tube includes runs, a return bend connecting the runs, and tangent points at junctures between the return bend and the runs. The return bend includes a bend angle and a controlled wrinkled portion. The controlled wrinkled portion is spaced from the tangent points along the serpentine circuit tube and has an angular extent about an inside of the return bend that is less than the bend angle. In this manner, the controlled wrinkled portion may be formed using a bend die having corresponding controlled wrinkle-forming features for less than the entire intrados of the return bend to permit the serpentine circuit tube to be slid out lengthwise from the bend die and increases the rapidity at which return bends may be formed in the serpentine circuit tube. In one embodiment, the controlled wrinkled portion includes ridges having amplitudes that are smaller adjacent the tangents points and increase as the wrinkled portion extends away from the tangent points to reduce resistance to fluid flow through the return bend and reduce the internal fluid pressure drop at the return bend relative to a non-tapered or non-eased configuration of the wrinkle ridges.
In another aspect, an indirect heat exchanger pressure vessel is provided that includes an inlet header to receive a pressurized working fluid, an outlet header, and a serpentine circuit tube connecting the inlet header and the outlet header to facilitate flow of the pressurized working fluid from the inlet header to the outlet header. The serpentine circuit tube includes a pair of runs and a return bend connecting the runs. The return bend includes an inner portion having a sinusoidal wave pattern at an intrados of the return bend, the sinusoidal wave pattern including peaks and valleys. The inner portion of the bend includes an arc pattern intersecting the sinusoidal wave pattern, the arc pattern comprising peak arcs intersecting the peaks and valley arcs intersecting the valleys. The intersecting sinusoidal wave pattern and arc pattern provide a smooth, continuously curving side wall of the serpentine circuit tube which strengthens the return bend against internal pressure. In one embodiment, the sinusoidal wave pattern has one or more end portions with shallower peaks and valleys and an intermediate portion with deeper peaks and valleys to reduce the internal fluid pressure drop across the return bend compared to a sinusoidal wave pattern having a constant peak and valley size.
The present disclosure also provides a closed circuit cooling tower including an indirect heat exchanger comprising a plurality of serpentine circuit tubes having runs and return bends connecting the runs. The return bends include wrinkled bends having controlled wrinkled portions. The closed circuit cooling tower comprises a fan operable to generate airflow relative to the serpentine circuit tubes and an evaporative liquid distribution assembly configured to distribute evaporative liquid onto the serpentine circuit tubes. The closed circuit cooling tower further comprises a sump to receive falling evaporative liquid from the serpentine circuit tubes and a pump operable to pump evaporative fluid from the sump back to the evaporative liquid distribution assembly. The controlled wrinkled bends strengthen the serpentine circuit tubes to withstand internal pressure from the working fluid within the serpentine circuit tubes during operation of the cooling tower. The controlled wrinkled bends also provide a constructive centerline radius of the wrinkled bends that is larger than the actual centerline radius of the controlled wrinkled bends and provides a reduced bend complexity factor compared to a return bend of a conventional serpentine circuit tube having the same outer diameter and wall thickness. The reduced bend complexity factor permits the controlled wrinkled bend to be bent without the use of an internal mandrel which simplifies the manufacturing process of the serpentine circuit tube.
Regarding
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The serpentine circuit tube 70 may be formed from a single straight tube that is bent at spaced locations along the tube to form the bends 84. The serpentine circuit tube 70 may be formed by progressively roll forming an elongated strip of material into a tubular shape and welding longitudinal edges of the elongate strip together to form a single weld running along the length of the serpentine circuit tube 70. In another approach, the serpentine circuit tube 70 may be made from a plurality of separately formed components. For example, the runs 79 may be separate components that are welded to the bends 84. Alternately the serpentine circuit tube 70 may be formed by welding separate lengths of tube together and then bending the longer welded tube. The serpentine circuit tube 70 may be made of a metallic material, such as carbon steel or stainless steel.
Regarding
The serpentine circuit tube 70 has a tube center line 102 extending through the runs 80, 82 and in the bend 84. The controlled wrinkled portion 94 is radially inward from the tube center line 102 and separated therefrom by a side surface portion 104. The smooth outer surface portion 98 and the side surface portion 104 permits the bend 84 to be stacked with bends of other serpentine circuit tubes in conventional arrangements as would a prior art tube having a smooth inner bend.
Referring to
The ridges 114 include end ridges 118, 120 that optionally have tapered lead-in portions 140, 142. The tapered lead-in portions 140, 142 provide a smooth transition between the relief portions 222, 224 and the sinusoidal wave pattern 110. The tapered lead-in portions 140, 142 smooth flow of the working fluid through the bend 84 and assists the material of the bend 84 to flow during bending. The tapered lead-in portions 140, 142, ridges 114, and grooves 116 reduce the internal fluid pressure drop caused by the working fluid flowing through the bend 84. Further, the tapered lead-end portion 140 facilitates better draining of the serpentine circuit tube 70. The bend 84 may have both tapered lead-in portions 140, 142 if the working fluid may flow through the bend 84 in either direction 143, 145. If the working fluid will only be flowing through the bend 84 in one direction 143, 145, the bend 84 may have only one tapered lead-in portion 140, 142.
Regarding
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The characteristics of the sinusoidal wave pattern 110 utilized for a given return bend may be selected for a particular application. For example, the number of ridges/grooves, amplitude, period, and/or one or more tapered lead-in portions may be selected for a particular application. The characteristics of the return bend may vary throughout the return bend, such as the amplitude and period varying throughout the return bend. The shape of the controlled wrinkled portion 94 as formed at least in part by two different intersecting cross-sectional profiles. Regarding
Returning to
Regarding
In another embodiment, the peak arc 152 and/or the valley arc 154 has a shape that is a portion of an ellipse. For example, the peak arc 152″ of
Regarding
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Referring again to
For example, a tube bend for a particular application may be provided with the following characteristic ratios:
Wherein OD refers to tube outer diameter, WT refers to wall thickness, and CLR refers to the bend centerline radius. Assuming that the values of these ratios for the tube bend are:
-
- W1=20 and D1=2 therefore CB1=10
Referring to Table 1 above, these values indicate that internal mandrel bending may be required if a conventional tube bender is used.
Now certain parameters of the bend are changed to show improved serpentine tube characteristics such as tighter bend radius for the same wall thickness, reduced coil weight, reduced internal fluid side pressure drop, reduced bend wall stresses, increased tube strength, increased tube stiffness, and/or increased heat transfer efficiency. These changes affect the characteristic ratios. For example, the new characteristic ratios may be selected as:
-
- W2=30 and D1=2 therefore CB2=15
The Bend Complexity characteristic ratio is now in the range where conventional tube benders can no longer compensate, and an internal mandrel is conventionally used to make this bend.
Internal mandrel bending is often undesirable for a variety of reasons as discussed above, making internal mandrel bending impractical for manufacturers that utilize long continuous lengths of tube to fabricate heat exchanger coils.
Referring again to
-
- W2=30 and D2=3 therefore CB2=10
Because the CB2 ratio is in the range of five to ten, the bend may be formed without an internal mandrel. However, simply increasing the bend CLR for a given application may not be acceptable because the new bend would be larger and occupy more space than the original bend. For example, the center-to-center distance between tube runs would be greater which means fewer tube runs could be fit into a certain envelop or coil height. Further, because each bend of the serpentine circuit tube would be taller, the serpentine circuit tube would have fewer runs for a given coil envelope or height which would reduce heat exchange capacity of the serpentine circuit tube. Reducing the number of runs of a serpentine circuit coil to increase the bend CLR is not an acceptable solution for many applications.
Referring again to
More specifically, the controlled wrinkled portion 94 provides a constructive bend center line 254 in the available space of the bend 84 thereby allowing for sufficient length along the inside of the bend 84 for the material to form the ridges 114 and grooves 116 in a controlled manner without buckling. The wrinkled portion 94 also maintains or improves other coil characteristics such as internal fluid pressure drop and heat transfer efficiency. Other characteristics of the bend 84 such as a reduction of the thinning of the wall on the extrados and overall stiffness of the bend 84 are also improved.
Referring to
The controlled wrinkled portion 94 provides advantages over conventional tube bends. For example, compared to other bends having wrinkles, the sinusoidal wave pattern 110 minimizes the stresses developed in the material of the tube 70 which allow for much higher internal fluid pressures. The ridges 114 and grooves 116, including the tapered lead-in portions 140, 142 may be sized to limit obstruction to the flow of fluid within the bend 84 and minimize internal fluid pressure drop through the bend 84. The sinusoidal wave pattern 110 increases the length of the material along the intrados 90 compared to a conventional bend having the same bend center line radius which increases the total surface area of the bend 84 and improves heat transfer efficiency by increasing fluid turbulence within the bend area. Further, the ridges 114 and grooves 116 operate as corrugated structure that stiffens the bend 84 as compared to a smooth, non-wrinkled bend. Still further, the controlled wrinkled portion 94 pushes the neutral axis of the bend 84 outward toward the extrados 92 of the bend 84 thereby reducing thinning of the material of the bend 84 along the extrados compared to a smooth, non-wrinkled bend.
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To compensate for the reduced vertical distance between the tangent points 122, 124, the material of the serpentine circuit tube 70 at the inside of the bend 84 is shaped to have the sinusoidal wave pattern 110. The sinusoidal wave pattern 110 has variables that define the shape of the sinusoidal wave pattern 110, such as the length of the sinusoidal wave pattern 110, number of peaks/valleys, period, and/or amplitude.
Referring now to
The sinusoidal wave pattern 110 is offset from the tangent points 122, 124 of the bend 84 by two portions of the serpentine circuit tube 70. The first portion is the relief portions 222, 224 corresponding to the offset angle, such as 7° on either side of the sinusoidal wave pattern 110, and measured between angles 220, 240 (see
The difference between the length 340 of the line 339 (see
Total arc length of sinusoidal pattern346=Intrados arc length340−Lengths342,344 (1.1)
Once the total arc length 346 of the sinusoidal wave pattern 110 is known, the total arc length 346 is divided by the number of peak portions 250A and valley portions 252A, such as in the range of 6 to 18 peaks and valleys, such as 8 to 12 peaks and valleys, to determine the arc length 350 for each peak portion 250A and valley portion 252A. Each peak portion 250A and valley portion 252A has a radius 349 and an arc length 350 given by:
Arc Length350=Radius349×θ (1.2)
Wherein θ is the angular extent of the peak portion 250A and valley portion 252A. The radius of each peak portion 250A and valley portion 252A may be determined using the following operations.
Referencing
The equation may be rearranged to be:
The relationship of a=r×θ may be substituted into equation 1.4 to result in:
At this point, the “a” value is known, i.e., the total arc length 346 of the sinusoidal wave pattern 110 divided by the number of peak portions 250 and valley portions 252 (
The foregoing equation may then be solved for theta using a numerical method such as Newton-Raphson iteration. Once theta has been determined, the radius of the peak portions 250A and valley portions 252A may be determined by solving for radius 349 in equation 1.2.
The radius 349 and theta permits the amplitude of the sinusoidal wave pattern 110 to be determined using the following equation:
Amplitude352=Radius349−(Radius349×cos θ)
It will be appreciated that ad-hoc adjustment to the sinusoidal wave pattern 110 may be utilized to tailor the sinusoidal wave pattern 110 for a particular application.
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In one embodiment, the continuously curving wrinkled surface 134 is perpendicular to a vertical plane that contains the peak arc 152, as well as a vertical plane that contains the valley arc 154. Referencing
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Various types of bends may be provided in accordance with the disclosure here. For example,
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With reference to
The wrinkled portion 902 is asymmetrical about a plane 908 that bisects the bend 900. Axes 915, 912 extend perpendicular to the plane 908 and intersect, respectively, the tangent points 913, 911. The tangent points 911, 913 are offset along the plane 908 a distance 910 such that the wrinkled portion 902 extends farther along the tube 896 on one side of the plane 908 than the other. The portion of the wrinkled portion 902 on the one side of the plane 908 (the upper portion in
The wrinkled portion 910 has an end groove 906A and an end ridge 904A. In one implementation, the end ridge 904A lacks a tapered lead-in portion. The offset portion 910A may provide a transition for flow in the tube 896 between the nearby straight 898 and the bend 900. Further, the end ridge 904B has a tapered lead-in portion 914 similar to various end ridges discussed above.
Regarding
The openings 1013, 1015 permit the bend die 1000 to have a tube fed into either opening 1013, 1015 of the bend die 1000 and allow the bend die 100 to be turned in the corresponding direction to form the bend 900 in the tube. For example and with reference to
The bend die 1000 is then turned in direction 1034 about axis 1036 while a trailing portion of the tube is supported by a pressure die. The bend die 1000 is turned in direction 1034 to impart the desired angular extent to the bend 900. Once the bend 900 has been formed, the bend die upper portion 1002 is shifted upward in direction 1033 and the tube is shifted relative to the bend die 1000 to position another portion of the tube in the bend die 1000 for bending. Continuing with the example, the tube is repositioned to advance a second portion of the tube into opening 1013, the bend die 1000 is closed, and the bend die 1000 is turned in a direction opposite direction 1034. The process of advancing and bending the tube is repeated until the desired number of bends have been imparted to the tube.
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The flattened cross-section of the tube 1100 may be, for example, an elliptical cross section. Regarding
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The flattened cross-section of the portions of the tube 1100 may be provided in a number of different approaches. For example, the tube bender used to bend the tube and impart the wrinkled portion 1104 may flatten the bend 1102 during the bending procedure. In another approach, the tube initially has an elliptical cross-section and the bending procedure imparts the wrinkled portion 1104 to the bend 1102 without further flattening of the tube. In yet another approach, a tube bender is used to form one or more bends of a tube and a press is used to flatten the tube after the bending procedure.
Uses of singular terms such as “a,” “an,” are intended to cover both the singular and the plural, unless otherwise indicated herein or clearly contradicted by context. The terms “comprising,” “having,” “including,” and “containing” are to be construed as open-ended terms. It is intended that the phrase “at least one of” as used herein be interpreted in the disjunctive sense. For example, the phrase “at least one of A and B” is intended to encompass A, B, or both A and B.
While there have been illustrated and described particular embodiments of the present invention, it will be appreciated that numerous changes and modifications will occur to those skilled in the art, and it is intended for the present invention to cover all those changes and modifications which fall within the scope of the appended claims. For example, the bends disclosed herein may be utilized in in various heat exchange apparatuses, such as an evaporative condenser, air cooled condenser, closed circuit fluid cooler, closed circuit cooling tower, open circuit cooling tower, dry cooler, ice thermal storage system, thermal storage coils, and/or a hydro-cooling coil, as some examples.
Claims
1. An indirect heat exchanger pressure vessel comprising:
- an inlet header to receive a pressurized working fluid;
- an outlet header to collect the pressurized working fluid;
- a serpentine circuit tube connecting the inlet and outlet headers and permitting the pressurized working fluid to flow from the inlet header to the outlet header;
- the serpentine circuit tube comprising runs and a return bend connecting the runs;
- the return bend having a controlled wrinkled portion; and
- the controlled wrinkled portion including alternating ridges and grooves.
2. The indirect heat exchanger pressure vessel of claim 1 wherein the inlet header, the outlet header, and the serpentine circuit tube are configured to operate at an internal pressure of at least 150 psig.
3. The indirect heat exchanger pressure vessel of claim 1 wherein the inlet header, the outlet header, and the serpentine circuit tube are configured to operate at an internal pressure of at least 410 psig.
4. The indirect heat exchanger pressure vessel of claim 1 wherein the inlet header, the outlet header, and the serpentine circuit tube are configured to operate at an internal pressure of at least 1200 psig.
5. The indirect heat exchanger pressure vessel of claim 1 wherein the serpentine circuit tube includes a pair of tangent points at junctures between the return bend and the runs of the serpentine circuit tube;
- the return bend having a bend angle;
- the controlled wrinkled portion of the return bend spaced from the tangent points along the serpentine circuit tube; and
- wherein the controlled wrinkled portion of the return bend has an angular extent about an inside of the return bend that is less than the bend angle.
6. The indirect heat exchanger pressure vessel of claim 1 wherein the controlled wrinkled portion of the return bend includes a sinusoidal pattern at an intrados of the return bend, the sinusoidal pattern including peaks at the ridges and valleys at the grooves of the bend.
7. The indirect heat exchanger pressure vessel of claim 6 wherein the controlled wrinkled portion of the return bend includes an arc pattern intersecting the sinusoidal pattern of the bend, the arc pattern comprising:
- peak arcs intersecting the peaks; and
- valley arcs intersecting the valleys.
8. The indirect heat exchanger pressure vessel of claim 7 wherein the peak arc has a first radius of curvature and the valley arc has a second radius of curvature, wherein the first radius of curvature and the second radius of curvature are substantially the same.
9. The indirect heat exchanger pressure vessel of claim 1 wherein the ridges include end ridges adjacent the runs of the serpentine circuit tube; and
- wherein at least one of the end ridges includes a tapered lead-in portion to smooth the flow of pressurized working fluid about the ridges and grooves.
10. The indirect heat exchanger pressure vessel of claim 1 wherein the return bend has a bend radius and includes a tubular side wall extending about an interior of the return bend;
- wherein the tubular side wall includes: a first semicircular inner wall portion at each ridge of the return bend, a first outer wall portion, and a pair of first connecting wall portions on opposite sides of the return bend interior connecting the first semicircular inner wall portion and the outer wall portion, wherein the first semicircular inner wall portion, outer wall portion, and the first connecting wall portions are radially aligned; and a second semicircular inner wall portion at each groove of the return bend, a second outer wall portion, and a pair of connecting wall portions on opposite sides of the return bend interior connecting the second semicircular inner wall portion and the second outer wall portion, wherein the second semicircular inner wall portion, second outer wall portion, and the second connecting wall portions are radially aligned.
11. The indirect heat exchanger pressure vessel of claim 10 wherein the first semicircular inner wall portion has a first radius of curvature and the second semicircular wall portion has a second radius of curvature that is substantially the same as the first radius of curvature.
12. The indirect heat exchanger pressure vessel of claim 10 wherein the first semicircular inner wall portion has a first angular extent and the second semicircular inner wall portion has a second angular extent, wherein the first angular extent and the second angular extent are each greater than 90 degrees.
13. The indirect heat exchanger pressure vessel of claim 12 wherein the first angular extent is greater than the second angular extent.
14. The indirect heat exchanger pressure vessel of claim 1 wherein the runs of the serpentine circuit tube comprise a plurality of pairs of runs; and
- wherein the return bend comprises a plurality of return bends connecting the pairs of runs.
15. The indirect heat exchanger pressure vessel of claim 1 wherein the return bend comprises:
- a first bend including a first controlled wrinkled portion of the controlled wrinkled portion;
- a second bend including a second controlled wrinkled portion of the controlled wrinkled portion; and
- a straight portion of the serpentine circuit tube connecting the first and second bends.
16. The indirect heat exchanger pressure vessel of claim 15 wherein the first bend has a first bend angle greater than or equal to 90 degrees and the second bend has a second bend angle less than or equal to 90 degrees.
17. The indirect heat exchanger pressure vessel of claim 1 wherein the return bend comprises a plurality of return bends; and
- wherein the return bends of the serpentine circuit tube have centerlines that are all coplanar.
18. The indirect heat exchanger pressure vessel of claim 1 wherein the return bend has a bend angle of 180 degrees and the controlled wrinkled portion of the bend has an arc length of less than or equal to 180 degrees
19. The indirect heat exchanger pressure vessel of claim 1 wherein the runs of the serpentine circuit tube include runs having a non-circular cross-sectional shape.
20. The indirect heat exchanger pressure vessel of claim 1 wherein the controlled wrinkle portion includes at least one tapered lead-in portion.
21. The indirect heat exchanger pressure vessel of claim 1 wherein the serpentine circuit tube has an outer diameter (OD), the serpentine circuit tube has a wall thickness (WT), and the return bend has a centerline radius (CLR); C B = OD 2 C L R × W T
- wherein the return bend has a bend complexity factor (CB) given by the following equation:
- wherein the bend complexity factor is greater than or equal to 10.
22. The indirect heat exchanger pressure vessel of claim 21 wherein the bend complexity factor is less than or equal to 20.
23. The indirect heat exchanger pressure vessel of claim 1 wherein the serpentine circuit tube includes a plurality of serpentine circuit tubes; and
- wherein the serpentine circuit tubes contact one another.
24. The indirect heat exchanger pressure vessel of claim 1 wherein the serpentine circuit tube includes a plurality of serpentine circuit tubes; and
- wherein the serpentine circuit tube return bends do not contact one another.
25. The indirect heat exchanger pressure vessel of claim 1 wherein the return bend of the serpentine circuit tube has a non-circular cross-sectional shape.
26. The indirect heat exchanger pressure vessel of claim 1 wherein the return bend of the serpentine circuit tube has an elliptical cross-sectional shape.
27. The indirect heat exchanger pressure vessel of claim 1 wherein the controlled wrinkled portion is asymmetrical about a plane bisecting the return bend.
28. The indirect heat exchanger pressure vessel of claim 1 wherein the return bend has a bend angle of 180 degrees; and
- wherein the controlled wrinkled portion is asymmetrical about a plane bisecting the return bend.
29. An indirect heat exchanger pressure vessel comprising:
- an inlet header to receive a pressurized working fluid;
- an outlet header to collect the pressurized working fluid;
- a serpentine circuit tube connecting the inlet and outlet headers to permit flow of pressurized working fluid from the inlet header to the outlet header, the serpentine circuit tube including runs and a return bend connecting the runs;
- the serpentine circuit tube having tangent points at junctures between the return bend and the runs, wherein the return bend comprises: a bend angle; a controlled wrinkled portion; the controlled wrinkled portion spaced from the tangent points along the serpentine circuit tube; and wherein the controlled wrinkled portion has an angular extent about an inside of the return bend that is less than the bend angle.
30. The indirect heat exchanger pressure vessel of claim 29 wherein the controlled wrinkled portion of the return bend includes ridges and grooves; and
- wherein the ridges include end ridges spaced from the tangent points.
31. The indirect heat exchanger pressure vessel of claim 29 wherein the controlled wrinkled portion of the return bend includes end ridges spaced from the tangent points; and
- at least one of the end ridges including a tapered lead-in portion to smooth working fluid flow about the wrinkled portion.
32. The indirect heat exchanger pressure vessel of claim 31 wherein the end ridges both include a tapered lead-in portion to smooth working fluid flow about the wrinkled portion.
33. The indirect heat exchanger pressure vessel of claim 29 wherein the controlled wrinkled portion of the return bend includes alternating ridges and grooves, the ridges and grooves having amplitudes that vary about the return bend.
34. The indirect heat exchanger pressure vessel of claim 33 wherein the ridges and grooves include a first plurality of ridges and grooves that increase in amplitudes as the first plurality of ridges and grooves extend away from one of the tangent points about the return bend.
35. The indirect heat exchanger pressure vessel of claim 34 wherein the ridges and grooves include a second plurality of ridges and grooves intermediate the first plurality of ridges and grooves and the other tangent point; and
- wherein the second plurality of ridges and grooves decrease in amplitude as the second plurality of ridges and grooves extends away from the first plurality of ridges and grooves toward the other tangent point.
36. The indirect heat exchanger pressure vessel of claim 29 wherein the controlled wrinkled portion of the return bend has an angular extent about the inside of the return bend that is at least five degrees less than the return bend angle.
37. The indirect heat exchanger pressure vessel of claim 29 wherein the serpentine circuit tube has an outer diameter (OD) and a wall thickness (WT); C B = OD 2 CCLR × WT 2
- wherein the return bend has a centerline radius and the controlled wrinkled portion of the return bend provides a constructive centerline radius (CCLR) of the return bend that is greater than the centerline radius; and
- the return bend has a bend complexity factor (CB) that is determined by the following relationship:
- wherein CB permits bending of the return bend without an internal mandrel.
38. The indirect heat exchanger pressure vessel of claim 37 wherein CB is approximately 10 or less.
39. The indirect heat exchanger pressure vessel of claim 29 wherein the serpentine circuit tubes each include an outer diameter (OD) and a wall thickness (WT), wherein:
- OD≥20×W.
40. The indirect heat exchanger pressure vessel of claim 29 wherein the inlet header, outlet header, and serpentine circuit tube are configured to operate at internal pressure of at least 150 psig.
41. The indirect heat exchanger pressure vessel of claim 29 wherein the inlet header, outlet header, and serpentine circuit tube are configured to operate at internal pressure of at least 410 psig.
42. The indirect heat exchanger pressure vessel of claim 29 wherein the inlet header, outlet header, and serpentine circuit tube are configured to operate at internal pressure of at least 1200 psig.
43. The indirect heat exchanger pressure vessel of claim 29 wherein the return bend comprises a first return bend adjacent one of the runs, a second return bend adjacent another run, and a connecting portion connecting the first bend and the second bend;
- wherein the bend angle comprises a first bend angle of the first bend and a second bend angle of the second bend;
- wherein the controlled wrinkled portion comprises a first controlled wrinkled portion of the first bend and a second controlled wrinkled portion of the second bend; and
- wherein the first wrinkled portion has a first angular extent about an inside of the first bend that is less than the first bend angle; and
- wherein the second controlled wrinkled portion has a second angular extent about an inside of the second bend that is less than the second bend angle.
44. The indirect heat exchanger pressure vessel of claim 29 wherein the bend angle is 180 degrees and the angular extent of the controlled wrinkled portion is less than 170 degrees.
45. The indirect heat exchanger pressure vessel of claim 29 wherein the return bend has a bend complexity factor greater than or equal to 10.
46. The indirect heat exchanger pressure vessel of claim 29 wherein the return bend has a bend complexity factor of less than or equal to 20.
47. An indirect heat exchanger pressure vessel comprising:
- an inlet header to receive a pressurized working fluid;
- an outlet header to collect the pressurized working fluid;
- a serpentine circuit tube connecting the inlet header and the outlet header to permit flow of the pressurized working fluid from the inlet header to the outlet header, the serpentine circuit tube including runs and a return bend connecting the runs, the return bend comprising:
- an inner portion having a sinusoidal wave pattern at an intrados of the return bend, the sinusoidal wave pattern including peaks and valleys;
- wherein the inner portion of the bend includes an arc pattern intersecting the sinusoidal wave pattern, the arc pattern comprising peak arcs intersecting the peaks and valley arcs intersecting the valleys.
48. The indirect heat exchanger pressure vessel of claim 47 wherein the peak arcs have a first radius of curvature and the valley arcs have a second radius of curvature; and
- wherein the peak arc first radius of curvature and the valley arc second radius of curvature are substantially the same.
49. The indirect heat exchanger pressure vessel of claim 47 wherein the peak arcs have an angular extent that is greater than an angular extent of the valley arcs.
50. The indirect heat exchanger pressure vessel of claim 47 wherein the serpentine circuit tube has a centerline;
- wherein the peak arcs each have a center radially inward of the centerline; and
- wherein the valley arcs each have a center radially outward of the centerline.
51. The indirect heat exchanger pressure vessel of claim 47 wherein the return bend has a midline plane, the sinusoidal pattern being in the midline plane;
- wherein the peak arcs are normal to the midline plane; and
- wherein the valley arcs are normal to the midline plane.
52. The indirect heat exchanger pressure vessel of claim 47 wherein the sinusoidal pattern includes end peak portions adjacent the runs; and
- wherein at least one of the end peak portions includes a tapered lead-in segment.
53. The indirect heat exchanger pressure vessel of claim 47 wherein the sinusoidal pattern has a period and an amplitude; and
- wherein at least one of the period and the amplitude varies about the return bend.
54. The indirect heat exchanger pressure vessel of claim 53 wherein the sinusoidal pattern includes a first minimum amplitude adjacent one of the runs, a second minimum amplitude adjacent another one of the runs, and a maximum amplitude intermediate the first and second minimum amplitudes along the intrados of the bend.
55. The indirect heat exchanger pressure vessel of claim 47 wherein the peak and valley arcs each have an angular extent of at least 100 degrees.
56. The indirect heat exchanger pressure vessel of claim 47 wherein the peak arcs each include a first radius of curvature and a second radius of curvature; and
- wherein the valley arcs each include a third radius of curvature and a fourth radius of curvature; and
- wherein the first radius of curvature and the third radius of curvature are substantially the same and the second radius of curvature and the fourth radius of curvature are substantially the same.
57. The indirect heat exchanger pressure vessel of claim 47 wherein the peak arcs have a shape defined by a portion of a first ellipse; and
- wherein the valley arcs have a shape defined by a portion of a second ellipse.
58. The indirect heat exchanger pressure vessel of claim 57 wherein the first ellipse has a first major dimension and a first minor dimension;
- wherein the second ellipse has a second major dimension and a second minor dimension; and
- wherein the first major dimension is substantially the same as the second major dimension and wherein the first minor dimension is substantially the same as the second minor dimension.
59. A closed circuit cooling tower comprising:
- an indirect heat exchanger comprising a plurality of serpentine circuit tubes comprising runs and return bends connecting the runs;
- the return bends including wrinkled bends having controlled wrinkled portions;
- a fan operable to generate airflow relative to the serpentine circuit tubes;
- an evaporative liquid distribution assembly configured to distribute evaporative liquid onto the serpentine circuit tubes;
- a sump to receive evaporative liquid from the serpentine circuit tubes; and
- a pump operable to pump evaporative fluid from the sump to the evaporative liquid distribution assembly.
60. The closed circuit cooling tower of claim 59 wherein the indirect heat exchanger includes an inlet header to receive pressurized working fluid and an outlet manifold to collect the pressurized working fluid;
- wherein the serpentine circuit tubes connect the inlet header and outlet header, the serpentine circuit tubes permitting flow of pressurized working fluid from the inlet header to the outlet header; and
- wherein the inlet header, the outlet header, and the serpentine circuit tubes are configured to operate at an internal pressure of at least 150 psig.
61. The closed circuit cooling tower of claim 59 wherein the return bends of each serpentine circuit tube includes a first wrinkled bend and the serpentine circuit tube includes tangent points at junctures between the first wrinkled bend and adjacent runs of the serpentine circuit tube;
- the first wrinkled bend having a bend angle;
- the controlled wrinkled portion of the first wrinkled return bend spaced from the tangent points along the serpentine circuit tube; and
- wherein the controlled wrinkled portion of the first wrinkled return bend has an angular extent about an inside of the first wrinkled return bend that is less than the bend angle.
62. The closed circuit cooling tower of claim 59 wherein the controlled wrinkled portions include a sinusoidal wave pattern at an intrados of the wrinkled bends, the sinusoidal wave pattern including peaks and valleys; and
- wherein the controlled wrinkled portions further include an arc pattern intersecting the sinusoidal wave pattern, the arc pattern comprising peak arcs intersecting the peaks and valley arcs intersecting the valleys.
63. The closed circuit cooling tower of claim 62 wherein the serpentine circuit tubes each have a centerline;
- wherein the peak arcs of each serpentine circuit tube have centers radially inward of the centerline of the serpentine circuit tube; and
- wherein the valley arcs of each serpentine circuit tube have centers radially outward of the centerline of the serpentine circuit tube.
64. The closed circuit cooling tower of claim 59 further comprising a direct heat exchanger, the evaporative liquid distribution assembly configured to distribute evaporative liquid onto the direct heat exchanger.
Type: Application
Filed: Jan 14, 2022
Publication Date: Jul 21, 2022
Inventors: Daniel E. Parker (Union Bridge, MD), Advait Damle (Columbia, MD), Frank T. Morrison (Crownsville, MD)
Application Number: 17/576,061